Presentation is loading. Please wait.

Presentation is loading. Please wait.

Introduction to Food Engineering

Similar presentations


Presentation on theme: "Introduction to Food Engineering"— Presentation transcript:

1 Introduction to Food Engineering
Psychrometrics Introduction to Food Engineering

2 Psychrometrics Thermodynamic properties of gas-vapor mixtures (air-water)

3 Properties of Dry Air Composition N2 78 %, O2 20.9 %
Standard dry air MW = Gas constant for dry air Ra = m3.Pa/kg.K

4

5 Properties of Dry Air Specific Volume Ra = gas constant
TA = absolute temperature (K) Pa = partial pressure of dry air

6 Properties of Dry Air Specific Heat (Cpa) Enthalpy (heat content)
At 1 atm ( kPa), T = - 40 – 60 C Average value kJ/kg.K Enthalpy (heat content) Reference 1 atm, 0 C

7 Properties of Dry Air Dry Bulb Temperature Indicated by sensor

8 Properties of Water Vapor
Moist air = dry air + water vapor Vapor in the air is superheated steam at low pressure & temperature Moist air is clear or foggy MW of water = Gas constant for water vapor Rw = m3Pa/kg.K

9 Properties of Water Vapor
Specific Volume of Water Vapor Below 66 C vapor follows ideal gas law

10 Properties of Water Vapor
Specific Heat of Water Vapor Within –71 to 184 C Cpw = 1.88 kJ/kg.K Enthalpy of water vapor Ta = dry bulb temp

11 Properties of Air-Vapor Mixtures
Gibbs-Dalton Law Up to 3 atm air-water mixtures follow perfect gas laws PB = barometric (total pressure) of moist air (kPa)

12 Dew-Point Temperature
Water vapors in air = steam at low pressure Saturation temperature = dew point Obtained from steam table at partial pressure exerted by water vapor Below this temp, condensation of moisture

13 Humidity Ratio Humidity Ratio (Moisture Content) or specific humidity, W (Kg water / ky dry air)

14 X = mole fraction

15 Relative Humidity Relative to maximum amount of moisture at dry bulb temperature

16 Relative Humidity Density
Density of water vapor/density of saturated vapor at dry bulb temp of air

17 Humid Heat Of air-water vapor mixture
Heat required to raise temp of 1 kg dry air + water vapor by 1 K (kJ/kg dry air . K) W = humidity ratio

18 Specific Volume Volume of 1 kg dry air + water vapor

19 Adiabatic Saturation of Air
Evaporation of water by sensible heat of entering air

20

21 Wet-Bulb Temperature Psychrometric wet bulb temperature
Movement of air Thermodynamic wet bulb temperature

22 The Psychrometric Chart

23 Example An air-vapor mixture is at 60 C dry bulb temp and 35 C wet bulb. Determine relative humidity, humidity ratio, specific volume, enthalpy and dew-point temp. RH = 20 %, W = kg/kg Enthalpy = 129 kJ/kg dry air Specific volume = 0.98 m3/kg dry air Dew-point temp = 29 C

24 Use of psychrometric chart
to evaluate complex air-conditioning processes Heating or Cooling of Air Humidity ratio constant

25 Example Calculate the rate of thermal energy required to heat 10 m3/s of outside air at 30 C dry bulb temp and 80 % RH to a dry bulb temp of 80 C Mass flow rate = vol flow rate/ specific vol

26 Mixing of Air Inverse proportion

27 Drying Adiabatic saturation process
Heat of evaporation is supplied only by drying air Dry bulb temp decreases, enthalpy constant ie. constant wet bulb Humidity ratio increases (gain moisture)

28

29 Example Heated air at 50 C, 10 % RH is used to dry rice. Air exits under saturated condition. Determine amount of water removed per kg of dry air. W1 = kg/kg Follow constant enthalpy line W2 = kg/kg Moisture removed = kg/kg

30


Download ppt "Introduction to Food Engineering"

Similar presentations


Ads by Google